Membrane distillation is an attractive technology for production of fresh water from seawater. The MemPower®MemPower® concept, studied in this work, uses available heat (86 °C) to produce pressurized water (2.2 bar and 46 °C) by membrane distillation, which again can be used to power a turbine for co-production of electricity. We develop a non-equilibrium thermodynamic model to accurately describe the transfer at the liquid-membrane interfaces, as well as through the hydrophobic membrane. The model can explain the observed mass flux, and shows that 85% of the energy is dissipated at the membrane-permeate interface. It appears that the system's performance will benefit from a lower interface resistance to heat transfer, in particular at the permeate side of the membrane. The nature of the membrane polymer and the pore diameter may play a role in this context.@en

Aqueous amino acid salt solutions that precipitate due to CO2 absorption are a relatively novel and promising class of solvents. Although the presence of solids in the process stream requires adequate measures related to slurry handling and crystallization control, precipitation also increases the solvent CO2 capacity and the energy performance of the stripper. By using an additional solid–liquid separation step to concentrate the slurry before it is sent to the stripper, known as the DECAB+ process, the energy performance can be further improved. Most of the current experimental work on these systems focuses on the amino acids taurine, α- and β-alanine, sarcosine, glycine, and proline, neutralized with equimolar amounts of potassium hydroxide. Investigated properties include the CO2 concentration at which precipitation is first observed, which is closely related to the solubility of the amino acid, the composition of the precipitate, and the CO2 absorption rate. The precipitate typically contains pure amino acids and/or bicarbonate, depending on the amino acid solubility. Shortcut process simulations have been used to estimate the energy performance of absorption processes using precipitating amino acids, so far focusing on 4M KOH + taurine (K-tau) and 4M KOH + α-alanine (K-α-ala) solutions. Specific regeneration duties below 2 GJ/ton CO2 seem possible for the DECAB+ process when using K-α-ala and lean vapor compressor (LVC). Compared to a conventional process using 30 wt % monoethanolamine and LVC, this corresponds to a reduction of 35% in the regeneration duty. Future research should focus on more-detailed process simulations, based on a predictive thermodynamic model that consistently describes the vapor–liquid–solid equilibria of the system. Demonstration of the DECAB+ process on a pilot scale is also highly recommended, with a special focus on the crystallization and slurry handling process steps and units@en

This article provides results of the in situ monitoring of carbon dioxide (CO2) removal under high pressure. An aqueous solution of methyldiethanolamine (MDEA) promoted by piperazine (PZ) for absorption rate acceleration was used. This system is promising for natural gas purification. A predictive statistical model was built using the chemometrics method and measurements of density, pH, conductivity, sound velocity, refractive index, and Near Infra-Red (NIR) spectroscopy. The CO2 capture rate ranged from 60% up to 96% at pressures in the absorber column ranging between 15 and 20 bar. The liquid stream composition was monitored at the low pressure part of a pileline at a location before a compressor stage. The concentrations of MDEA, PZ, and CO2 were predicted in-line using different sets of the measurement devices during 3 days of the measurement campaign. The developed approach allowed for prediction of the concentrations with accuracies of 0.7% for MDEA, 0.4% for PZ, and 2.5% for CO2.@en

This article provides results of the in situ monitoring of carbon dioxide (CO2) removal under high pressure. An aqueous solution of methyldiethanolamine (MDEA) promoted by piperazine (PZ) for absorption rate acceleration was used. This system is promising for natural gas purification. A predictive statistical model was built using the chemometrics method and measurements of density, pH, conductivity, sound velocity, refractive index, and Near Infra-Red (NIR) spectroscopy. The CO2 capture rate ranged from 60% up to 96% at pressures in the absorber column ranging between 15 and 20 bar. The liquid stream composition was monitored at the low pressure part of a pileline at a location before a compressor stage. The concentrations of MDEA, PZ, and CO2 were predicted in-line using different sets of the measurement devices during 3 days of the measurement campaign. The developed approach allowed for prediction of the concentrations with accuracies of 0.7% for MDEA, 0.4% for PZ, and 2.5% for CO2.@en

This article provides results of the in situ monitoring of carbon dioxide (CO2) removal under high pressure. An aqueous solution of methyldiethanolamine (MDEA) promoted by piperazine (PZ) for absorption rate acceleration was used. This system is promising for natural gas purification. A predictive statistical model was built using the chemometrics method and measurements of density, pH, conductivity, sound velocity, refractive index, and Near Infra-Red (NIR) spectroscopy. The CO2 capture rate ranged from 60% up to 96% at pressures in the absorber column ranging between 15 and 20 bar. The liquid stream composition was monitored at the low pressure part of a pileline at a location before a compressor stage. The concentrations of MDEA, PZ, and CO2 were predicted in-line using different sets of the measurement devices during 3 days of the measurement campaign. The developed approach allowed for prediction of the concentrations with accuracies of 0.7% for MDEA, 0.4% for PZ, and 2.5% for CO2.@en